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book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
Exercise 11
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell
bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate
is glucose, and its concentration in the feed bulk liquid phase is
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:   The nutrient flow
rate is F = 2 l/min. The particle size of Ca-alginate beads is
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:   = 0.5 cm. The rate constants
for this conversion are
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:
for the following rate expression:
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:
The surface area of the alginate beads per unit volume of the reactor is
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:   and
the cross-sectional area of the bed is
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:   Assuming a first-order reaction-kinetics
(e.g., relatively low substrate concentrations), determine the required bed height for 80% con-
version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we
can use the following equations:
5 The bioconversion of glucose to ethanol is carried out in a packed-bed, immobilized-cell bioreactor containing yeast cells entrapped in Ca-alginate beads. The rate-limiting substrate is glucose, and its concentration in the feed bulk liquid phase is    The nutrient flow rate is F = 2 l/min. The particle size of Ca-alginate beads is    = 0.5 cm. The rate constants for this conversion are     for the following rate expression:     The surface area of the alginate beads per unit volume of the reactor is    and the cross-sectional area of the bed is    Assuming a first-order reaction-kinetics (e.g., relatively low substrate concentrations), determine the required bed height for 80% con- version of glucose to ethanol at the exit stream. Hint: To calculate the effectiveness factor, we can use the following equations:
Explanation
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Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler
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